(19)
(11) EP 0 003 404 A1

(12) EUROPEAN PATENT APPLICATION

(43) Date of publication:
08.08.1979 Bulletin 1979/16

(21) Application number: 79300073.8

(22) Date of filing: 17.01.1979
(51) International Patent Classification (IPC)2B32B 27/30, B32B 27/08, B65D 65/40
(84) Designated Contracting States:
FR GB

(30) Priority: 18.01.1978 US 870599

(71) Applicant: UNION CARBIDE CORPORATION
Danbury Connecticut 06817 (US)

(72) Inventors:
  • Lustig, Stanley
    Park Forest Illinois 60466 (US)
  • Vicik, Stephen James
    Darien Illinois 60559 (US)

(74) Representative: McCall, John Douglas et al
W.P. THOMPSON & CO. Coopers Building Church Street
Liverpool L1 3AB
Liverpool L1 3AB (GB)


(56) References cited: : 
   
       


    (54) Multi-layer plastics film suitable for use as a packaging bag


    (57) An elastic multilayer film suitable for use in connection with the packaging of poultry, comprises a first outer layer including a plasticized polyvinyl chloride having an inherent viscosity greater than about 1.10 and having a plasticizer content of from about 35 phr to about 40 phr, and a second outer layer including an ethylene vinyl acetate copolymer having a vinyl acetate content of from about 16% to about 20% by weight and having a melt flow of from about 1.0 to about 3.0 decigrams per minute.


    Description


    [0001] The present invention relatec to an elastic aultilayer film, and mere particularly to a two-layer film suitable for use in the packsging of poultry.

    [0002] Generally, one of the typical commtrcial packeging operations of frozen poultry includes the following steps:

    1. Enclosing boneless turkey meat in a string betting;

    2. Enclosirg the netted turkey meat in an elastic bag by mechanically expanding the bag to aaproxi- mately 140% of its normal circumference, placing the netted turkey meat in the bag, and thereafter, sllowing the bag to relax to its normal size to form a tight package;

    3. Generally evacuating the air from the bag and clipping the end of the bag closed;

    4. Quick freezing the bagged turkey meat to a temperature as low as about -40° C; and

    5. Shipping the frozen turkey meat in the bag.



    [0003] A bag suitable for these steps must be formed from a film exhibiting good dimensional stability, praduction controllable thickness, non-tacky surfaces, and economical production. In addition, the film mist have good resictance to abrasion and impact because the shipping of the bagged turkey meat usually results in the abrasion of bags sgainst each other as well as their mutual impacts.

    [0004] One prior art file used to fabricate bags for the turkey meat is a plasticized vinyl film. The bags formed from this film have the dravback that an unsaticfactory percentage of bags became damaged during the shipping step.

    [0005] In accprdaoce with the present invention, there is provided an elastic multilayer film suitable far use in connection with the packaging of poultry, comprising a first outer layer including a plasticired polyvinyl chloride having an inherent viscosity greater than about 1.10 and having a plasticizer content of from about 35 phr to about 40 phr, and a second outer layer including an ethylene vinyl acetate copolymer having a vinyl acetate content of from about 16% to about 20% by veight and beving a melt flow of from about 1.0 to about 3.0 decigrams per minute. Preferably, the first outer layer has a thickness of from about 1.75 mils to about 2·0 mils and the second outer layer has a thickness of from about 0.5 mil to about 0.75 mil.

    [0006] Praferably, the film consiats of the two outer layers. In addition, a thickness of 0.75 mil for the second outer layer and vinyl acetate content of about 18% by veight are preferable.

    [0007] Preferably, the plasticizer is at least 27 phr of a food approved plasticirer such as dibutyl sebacate or a di-n-hexyl azelate which are low temperature plasticirers. The remainingplisticizer is preferably an epoxidized soybean oil.

    [0008] An ethylene vinyl acetate copolymer having a vinyl acetate content greater than about 20% by weight generally results in a film having insufficient strength. For a vinyl acetate content less than about 16% by weight, there is poor adhesion between the two outer layers.

    [0009] An ethylene vinyl acetate copolymer having a selt flow less than about 1.0 decigram per minute is undesirable because of the difficulty in processing this type of resin at die temperatures preferable for plasticized pclyvinyl chloride extrusion. A melt flow too high tends to weaken the puncture resistance of the film.

    [0010] Generally, the processes of forming the film of the invention and bags can be carried but using conventional blown film extrusion processes.

    [0011] Preferably, a two-layer film is coextruded into tubular form, air cooled to a temperature below the softening point, and then wound into rolls for subsequent iabrication into bags. It has been discovered that the temperatures of the elbow end die of the extrusion device are critical for obtaining satisfactory films according to the invection and these temperatures must be adjusted so that the temperature of the inside of the extruded tube of file and the temperature between the two layers is relatively cool. These temperatures are readily identifiable tc persons in the art because the film leaving the extrusion device has a visual appearance of having a low gloss level. The preferred conditions correspond to a temperature of about 425" F at the exit of the die.

    [0012] Illustrative, non-limiting examples of the practice of the invention are set out below. Fumerous other examples can readily be evolved in the light of the guiding principles and teachings contained herein. The examples given herein are intended mainly to illustrate the invention and not in any sense to linte the manner in which the invention can be practiced.

    [0013] All percentages and parts stated herein are by weight unless otherwise stated.

    [0014] As used berein, the term "phr" has the conventional meaning of parts per 100 parts of polymer.

    [0015] The materials described herein have their properties determined in scordapce with the following test methods:

    Melt Flow - ASTM D-1238 -57T at 44 psi and 190°C

    Viscosity - ASTH D-1243



    [0016] In the examples, the meterials shown in Trbles 1 and 2 were employed:




    Examples 1 to 9



    [0017] Two layer films were produced with a first outside layer of a plasticized polyvinyl chloride including 27.5 phr of dibutyl sebscate and 10.0 phr of epoxidized soybean oil, and a second outer layer of an ethylene vinyl acetate co- polymer as shown in Table 3.

    [0018] Generally, the extrusion equipment includes a 2-1/2 inch 16:1 L/D HRM oil bsated extruder to feed the plesticized polyvinyl chloride. The barrel temperature was

    maintained at about 300° F and the screw speed was about 22 rpm. The ethylene vinyl acetate extruder was a 1-1/4 inch - 18:1 L/D TEC extruder with the barrel teaperature maintained at about 320° F and a screw apeed of about 34 rpm. A 60 mm diameter two layer die was used with the plasticized vinyl chloride as the inner layer and the ethylene vinyl acetate capolymer as the outer layer. The die base temperatures were maintained at about 425° F while the exit temperature veried from about 425° F to about 475° F. Conventional blown film methods were used to cool and flatten the bubble. The film speed was about 50 fpm.

    [0019] For the examples 1 to 9, the EVA's A, B, C, D, and E were used as well as different layer thicknesses. Observätions on the extrusion performance and layer adhesion are indicated in addition to varions physical properties of the films. The TITE-WRAP test is a test especially relevant to the intended use of the film of the invention. The tubular film is cut to a length of about one foot long and powdered to reduce its coefficient of friction and placed on two sets of jews which are connected to pneumatic cylinders. The jaws are rapidly opened to that the circumference of the film is increased by about 50%.

    [0020] Although EVA's C and D showed acceptable results for the respective examples 5 and 7, the unsatisfactory results of the related examples 6 end 8 indicate that the layer thicknesses suitable for conmercial use night be unreliable. The EVA E presented problems in the extrusion because of the high viscosity, as indicated by the relatively low melt flow, is untatisfactory at the temperatures tuitable for vinyl extrusion.

    [0021] The EVA's A and B showed satisfactory performince in the propertice tested. Surprisingly, a film hiving a second outer layer about 0.5 mil in thickness was stronger then a film having a second outer layer about 1.0 mil in tnickness.

    Examples 10 to 17



    [0022] Examples 10 to 17 were carried out with an endeavor to produce a film using conventional methods in order to compare the perfortance of additional polymers for the second outer laper. The first outer layer was the same as the example 1.

    [0023] Table 4 shows the results of the examples 10 to 17. None of these examples produced a film satisfactory for commercially packaging poultry.

    [0024] Examples 18 to 21

    [0025] Examples 18 to 21 were carried out to demonstrate the necessity of maintaining the extrusion conditions relatively cool.

    [0026] The example 18 is a known single layer plesticired vinyl used for packaging poultry. The examples 19 to 21 are films of the inventions with the dimensions shown and comprising the materials of the example 1. Also shown in the Table 5 are the extrusion conditions for the films and the breakage during packaging and shipping of bags fabricated from the films.





    [0027] The Table 5 shows the superior performance of the film according to the invention and the importance of the extrusion temperature on bag performance.

    Examples 22 to 40



    [0028] Examples 22 is a conventional single layer film of plasticized vinyl and examples 23 to 40 are films with the materiels of the example 1 prepared under various conditions and different layer thicknesses as shown in Table 6.

    [0029] Generally, the temperatures of the inside of the tubular film and between the layers can be estimeted by a person having prdinary skill in the art by visual appearance (glase) on the film. Temperatures at the exit of the die which are broadly referred to as "cold", "warm", and "not" correspond respectively to about 425°F, about 450° F, and about 475° F.

    [0030] The single layer film of the example 22 was included to provide a comparison to the prior art.

    [0031] The Dynamic Tensile test includes cycling a sample to a 50 inches per minute jaw speed from 0 to 200% elongation at about -40° F and recording the average number of cycles to failure.

    [0032] The film condition was visually determined based on the gloss of the film.



    [0033] The plasticized polyvinyl chloride in the examples 23 to 38 was the same as in the previous examples. In the examples 39 and 40, the plasticizer was 30 phr dibutyl sebacate.

    [0034] The examples 24 to 28 show that reducing the temperature of the extrusion system pravides an improved tensile strength.

    [0035] The examples 29 to 35 generally were run at relatively cool extrusion temperatures and provide a comparison between films having layers of different thicknesses. While the impact strength of each of the examples 32 and 33 was high, the dynamic tensile strength for each was low.

    [0036] For the examples 36 to 40, the thickness of the first puter layer was varied slong with the smount of plasticizer. These examples provided the best results for both the dynamic tensile and the impact strength tests.

    [0037] We wish it understood that we do not desire to be limited to the exact details shown and described, for obvious modifications will occur to a person skilled in the art.


    Claims

    1. An elastic multilayer film suitable for use in connection vith the packaging of poultry, comprising a first outer layer including a plasticized polyvinyl chloride having an inherent viscosity greater than about 1.10 and having a plasticizer content of from about 35 phr to sbout 40 phr; and a second outer layer including an ethyleae vinyl acetate copolymer having a vinyl acetate content of from about 16% to about 20% by weight and having a melt flow of from about 1.0 to about 3.0 decigrams per minute.
     
    2. A film as claimed in clxim 1, wherein said first outer layer has a thickness of from about 1.75 mils to about 2.0 mils and said second outer layer has a thickness of from about 0.5 mil to about 0.75 mil.
     
    3. A film as claimed in claim 1 or 2, wherein the vinyl acetate is about 18% by weight.
     
    4. A film as claimed in any one of the preceding claims, wherein said layers are in physical contact with each other.
     
    5. A film as claimed in any one of the . preceding claims, wherein said second outer layer has a thickness of about 0.75 mil.
     
    6. A film as claimed in any one of the preceding claims, wherein said plasticizer is at least about 27 phr.
     
    7. A film as claimed in any one of the preceding claims, wherein said plasticizer includes dibutyl sebacate.
     
    8. A film as claimed in any one of claims 1 to 6, wherein said plasticizer includes di-n-hexyl azelate.
     
    9. A film as claimed in claim 7 or 8, wherein any additional amount of said plasticizer includes epoxidized soybean oil.
     
    10. A film as claimed in any one of the preceding claims, wherein said melt flow is about 1.0 decigram per minute.
     
    11. A bag fabricated from a film as claimed in any one of the preceding claims.
     





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